EP1260485B1 - Vorrichtung zur biologischen Fluidbehandlung - Google Patents
Vorrichtung zur biologischen Fluidbehandlung Download PDFInfo
- Publication number
- EP1260485B1 EP1260485B1 EP20010112677 EP01112677A EP1260485B1 EP 1260485 B1 EP1260485 B1 EP 1260485B1 EP 20010112677 EP20010112677 EP 20010112677 EP 01112677 A EP01112677 A EP 01112677A EP 1260485 B1 EP1260485 B1 EP 1260485B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- microorganisms
- disks
- stack
- disk
- discs
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/10—Packings; Fillings; Grids
- C02F3/101—Arranged-type packing, e.g. stacks, arrays
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Definitions
- the invention relates to a device for biological fluid treatment according to the features specified in the preamble of claim 1.
- carrier biologies d. H. to microorganisms which are fixed on a carrier material with a large surface, along which the fluid to be treated is guided.
- carrier biologies d. H. to microorganisms which are fixed on a carrier material with a large surface, along which the fluid to be treated is guided.
- Such a method is known, for example, from EP 0 470 931 A2.
- microorganism-affected surfaces One problem with these microorganism-affected surfaces is that the surface activity changes with increasing layer thickness, since with increasing layer thickness, the underlying microorganisms are supplied less well and thus can participate less actively in the process. The excess microorganisms are therefore at regular intervals from the surfaces to remove and remove the settling sludge, which is usually done by backwashing.
- a device for biological fluid treatment in which the fluid flows through a trough, in which two rotating disc stacks dive on the discs microorganisms are arranged, which are used for wastewater treatment.
- the water flows through the trough-shaped basin substantially in the axial direction of the disk stack, so that the individual disks are flowed around in succession.
- the present invention has the object of providing a generic device in such a way that it works effectively with the smallest possible size and beyond limits the growth of microorganisms to reliably.
- the surfaces form parts of disks or disk packages, which are arranged substantially parallel to one another and overlapping, so that when appropriate Choice and arrangement of plates and drive results in an extremely compact design, in which also the excess part of the microorganisms can be removed continuously.
- the surfaces are advantageously formed by lying in the discs grooves and the fluid passed through these grooves.
- the grooves are open towards the opposite disc, so that this opposite disc together with the groove forms a channel for fluid transfer.
- the discs are preferably annular, so that a central fluid supply through the inner recess of the plate stack and the removal can be done on the outside or vice versa.
- the grooves are substantially radially or at least radially directed, for example, so that the groove bounding edges of opposing discs are arranged so that they always meet at rotation in the same angle to each other.
- the device is hermetically sealed or integrable in a hermetically sealed line system so that it can be pressurized with a reaction-promoting gas, for example air, in order to accelerate an aerobic reaction process.
- the excess part of microorganisms is mechanically released from the afflicted surface and removed via the fluid flow.
- the running reaction process is controlled much more precisely than in devices according to the prior art. It is important to obtain a basis for growth for the further microbiological process.
- the surfaces on which the microorganisms accumulate are preferably structured from a porous or roughened material and / or in their surface.
- Mechanical release of the excess portion of microorganisms from the surface may also be accomplished utilizing centrifugal force. It is possible to vary the layer thickness of the microorganisms by the drive speed is varied accordingly. The higher the rotational speed of the rotational body, the more microorganisms are removed due to centrifugal force, and the thinner the layer thickness of the microorganisms will be.
- microorganism-afflicted surfaces are parts of discs or disc pacts which are arranged substantially parallel to one another and overlapping, so that with a suitable choice and arrangement of plates and drive results in an extremely compact design, in which also the excess part of the microorganisms continuously can be removed.
- a principle is shown how by deformation of surfaces excess microorganisms can be removed.
- two elastic, substantially flat extending body 1 which have on opposite sides surfaces 2, which are provided for the adhesion of microorganisms.
- the mutually facing sides of the body 1 are provided with triangular grooves 3 in cross-section, such that opposite grooves 3 each form an approximately square in cross-section channel 4.
- the microorganisms afflicted surfaces 2 limit the channels 4, wherein the fluid to be treated is passed through the channels 4.
- the fluid flows along the channels 4 and thereby reacts with the adhering to the surfaces 2 microorganisms 5 (Fig. 2).
- the flow cross-section of the channels 4 decreases, as shown by way of example in FIG. 2a.
- the excess microorganisms must be removed to ensure the functioning of the device.
- the surfaces 2 are deformed by pressing the bodies 1 against one another such that the constellation shown in FIG. 2b results, at which the microorganisms 5 of opposing grooves 3 abut one another.
- the above-described movement of the body 1 to each other can either by pressurization of the backs and / or Switzerlandbeetzschung across the Grooves 3 done.
- the body 1 deform elastically into the position shown in Fig. 2b.
- the channels 4 are directed again, wherein the excess microorganisms 5 are removed from the channels 4 during renewed fluid flow, whereby the desired layer thickness of microorganisms is restored.
- the body 1 has the same shape as in the embodiment illustrated with reference to FIG. 1, but is not arranged in pairs. Also there triangular grooves 3 are provided in cross section, the walls of which form surfaces 2 to which microorganisms 5 adhere. The fluid flows along the surfaces 2 in the direction of Nutverlaufs here. Again, the layer thickness of the microorganisms 5 increases over time.
- a mechanical scraper 6 is provided, which is movable along the upper side of the body 1 by means of, for example, an electric, hydraulic or pneumatic drive and mechanically peels off the part of the microorganisms 5 projecting beyond the upper side of the body 1 , By the mechanical scraper 6 here the layer thickness of the microorganisms 5 is set. The removal of the separated microorganisms 5 takes place by means of the fluid.
- the surfaces 2 illustrated with reference to FIGS. 1 and 2 or 3, which are freed of excess microorganisms according to the principles explained above, are arranged in a suitable closed and hermetically sealable container, as shown by way of example in FIG. 4.
- the container to accelerate the microbiological process can be pressurized.
- a container 7 in which a stack of spaced and parallel to each other arranged discs 8 is arranged on a hollow shaft 9 which is rotatably driven by a motor 10 arranged outside the container 7.
- the interior of the hollow shaft 9 is available an inlet channel II in connection, via which the fluid to be treated passes into the container 7. It then flows through a plurality of recesses 12 in the hollow shaft 9 between the discs 8 to the outside to leave the container after treatment via an outlet channel 13.
- the discs 8 form with their top and bottom surfaces 14, which are afflicted with microorganisms.
- the package of discs 8 is rotatably driven via the hollow shaft 9 by means of the motor 10. This can be done continuously or discontinuously, in each case only for removing excess microorganisms. Depending on the rotational speed of the motor 10, a layer thickness determined in accordance with the centrifugal forces acts, which can drop off from the center towards the edge.
- the embodiment of the invention shown with reference to FIGS. 5 to 8 likewise has a container 15 with inlet channel 11 and outlet channel 13.
- two intermeshing disc stacks 16 and 17 of parallel and spaced apart annular discs 18 and 19 are provided within the container 15.
- the discs 19 are secured by means disposed on the outside of the stack fastening bolts 21 on a common carrier 22 via diametrically arranged on the outer periphery projections 20 which is connected by means of a shaft 23 with an outside of the container 15 arranged motor 10
- the discs 19 (Fig. 6) of the other disc stack 17 on the inner periphery projections 24 which are fixed via fastening bolts 25 on a common carrier 26 and at the bottom of the container 7.
- the discs 18 and 19 each have on both sides grooves 27, which have a substantially rectangular cross-section and are directed substantially radially, but at different angles, as shown in FIG.
- the discs 18 and 19 are within the stack 16 and 17 so far away arranged that the grooves 27 of a disc are channel-forming completed by the adjacent disc, the discs, however, remain easily movable to each other.
- the grooves 24 form surfaces 28 adhere to microorganisms, so that the two disk stacks 16 and 17 form a plurality of channels with a comparatively large active surface with a small size.
- the discs 18 and 19 can be inexpensively manufactured as plastic injection molded parts. The flow through the container takes place from the inlet channel 11 through the grooves 27 between the disk stacks 16 and 17 into the free center to the outlet channel 13.
- microorganisms forming on the surfaces 28 with increasing layer thickness during operation of the device are removed here mechanically and preferably continuously by rotation of the shaft 23. While the plate stack fixed to inner projections 24 is fixed, the plate stack fixed to the outer projections 20 rotates, the edges 29 of the grooves 27 acting as scrapers and loosening excess microorganisms, which are then carried over the fluid flowing through and thus removed.
- the discs 30 and 31 show an alternative stacking arrangement, which comb in the same manner as described above with reference to the disc stacks 16 and 17 with each other.
- the disk 30 ( Figure 9) is provided with a plurality of short but comparatively small cross-section and substantially radial channels provided in a projection extending approximately radially on the disk.
- the discs 31 have channels which are arranged spirally. With a combination of these discs 30 and 31 results in a very constant layer thickness of microorganisms, wherein the grooves of the discs 30 form the essential flow path, whereas the edges of the grooves of the discs 31 perform substantially the task of stripping.
- This arrangement of discs 30 and 31 has very good sliding properties, so that comparatively high slice stacks can be formed.
- Figs. 4 and 5 illustrate substantially the principal device structure
- Fig. 11 shows how such a device may look in practice. It can here a standard motor 10 are used with downstream gear 32, is flanged to the same axis in container 33, which is substantially tubular and may have a length of for example one meter. Within this pipe section 33, the disk stacks are arranged. The hydraulic connection of the device takes place at the lower end by means of two inline flanges 34 and 35 as inlet and outlet.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Biological Treatment Of Waste Water (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- External Artificial Organs (AREA)
Priority Applications (11)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT01112677T ATE337273T1 (de) | 2001-05-25 | 2001-05-25 | Vorrichtung zur biologischen fluidbehandlung |
EP20010112677 EP1260485B1 (de) | 2001-05-25 | 2001-05-25 | Vorrichtung zur biologischen Fluidbehandlung |
DE50110806T DE50110806D1 (de) | 2001-05-25 | 2001-05-25 | Vorrichtung zur biologischen Fluidbehandlung |
RU2003137225A RU2299865C2 (ru) | 2001-05-25 | 2002-05-24 | Устройство для биологической обработки жидкости |
JP2002591401A JP4632630B2 (ja) | 2001-05-25 | 2002-05-24 | 生物学的流体処理デバイス |
AU2002339028A AU2002339028B2 (en) | 2001-05-25 | 2002-05-24 | Device for biological fluid treatment |
US10/479,209 US7105085B2 (en) | 2001-05-25 | 2002-05-24 | Device for biological fluid treatment |
PCT/EP2002/005749 WO2002094724A1 (de) | 2001-05-25 | 2002-05-24 | Vorrichtung zur biologischen fluidbehandlung |
PL368274A PL207367B1 (pl) | 2001-05-25 | 2002-05-24 | Urządzenie do biologicznej obróbki płynu |
EP02743096A EP1390305A1 (de) | 2001-05-25 | 2002-05-24 | Vorrichtung zur biologischen fluidbehandlung |
CA002446830A CA2446830C (en) | 2001-05-25 | 2002-05-24 | Device for biological fluid treatment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP20010112677 EP1260485B1 (de) | 2001-05-25 | 2001-05-25 | Vorrichtung zur biologischen Fluidbehandlung |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1260485A1 EP1260485A1 (de) | 2002-11-27 |
EP1260485B1 true EP1260485B1 (de) | 2006-08-23 |
Family
ID=8177540
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP20010112677 Expired - Lifetime EP1260485B1 (de) | 2001-05-25 | 2001-05-25 | Vorrichtung zur biologischen Fluidbehandlung |
EP02743096A Withdrawn EP1390305A1 (de) | 2001-05-25 | 2002-05-24 | Vorrichtung zur biologischen fluidbehandlung |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP02743096A Withdrawn EP1390305A1 (de) | 2001-05-25 | 2002-05-24 | Vorrichtung zur biologischen fluidbehandlung |
Country Status (10)
Country | Link |
---|---|
US (1) | US7105085B2 (ru) |
EP (2) | EP1260485B1 (ru) |
JP (1) | JP4632630B2 (ru) |
AT (1) | ATE337273T1 (ru) |
AU (1) | AU2002339028B2 (ru) |
CA (1) | CA2446830C (ru) |
DE (1) | DE50110806D1 (ru) |
PL (1) | PL207367B1 (ru) |
RU (1) | RU2299865C2 (ru) |
WO (1) | WO2002094724A1 (ru) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
PL1616621T3 (pl) * | 2004-07-14 | 2011-11-30 | Grundfos As | Urządzenie do obróbki płynów |
EP1717208B1 (de) | 2005-04-28 | 2013-06-26 | Grundfos Management A/S | Vorrichtung zur Fluidbehandlung, insbesondere Abwasserbehandlung, mit einem Scheibenstapel |
EP1854764B1 (de) * | 2006-05-10 | 2016-12-14 | Grundfos Management A/S | Reaktor mit Filterplattenstapel |
EP2483209A4 (en) * | 2009-09-09 | 2014-05-21 | Septicosol Inc | APPARATUS FOR WASTEWATER TREATMENT |
EP2733118A1 (en) * | 2012-11-16 | 2014-05-21 | New Century Membrane Technology Co., Ltd. | Water treatment apparatus |
JP6111058B2 (ja) * | 2012-12-07 | 2017-04-05 | 東洋鋼鈑株式会社 | 燃料電池用セパレータ、燃料電池セル、燃料電池スタック、および燃料電池用セパレータの製造方法 |
RU2555881C2 (ru) * | 2013-08-21 | 2015-07-10 | Общество с ограниченной ответственностью НАУЧНО-ПРОИЗВОДСТВЕННАЯ ФИРМА "ЭТЕК ЛТД" | Плавающий полимерный элемент загрузки для биологической очистки сточных вод |
DE102015015945A1 (de) * | 2015-12-08 | 2017-06-22 | Gea 2H Water Technologies Gmbh | Tropfkörper und Drehsprenger für einen Tropfkörper |
CN110627214B (zh) * | 2019-08-15 | 2022-02-18 | 西安建筑科技大学 | 一种改善管道内有毒气体的装置和方法 |
Family Cites Families (30)
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GB1178601A (en) * | 1967-01-05 | 1970-01-21 | Nat Res Dev | Biological Treatment of Waste Water containing Organic Matter |
US3335081A (en) * | 1966-02-02 | 1967-08-08 | El-Naggar Ahmed Sami | Method of treatment of sewage by biooxidation and apparatus therefor |
GB1401000A (en) * | 1971-12-08 | 1975-07-16 | Nat Res Dev | Biological treatment of waste water containing organic matter |
US3598726A (en) * | 1968-08-27 | 1971-08-10 | Autotrol Corp | Water treatment apparatus and method |
DE2235470C3 (de) * | 1972-07-20 | 1974-12-05 | Maschinenfabrik Hellmut Geiger, 7500 Karlsruhe | Verfahren zum Betreiben eines Tropfkörpers und Tropfkörper zur Durchführung des Verfahrens |
US4162195A (en) * | 1974-04-04 | 1979-07-24 | Aktiebolaget Kalle-Regulatorer | Biological testing device and method of measuring toxicity of sewage |
SE381935B (sv) * | 1974-04-04 | 1975-12-22 | Kaelle Regulatorer Ab | Apparat for metning av akuttoxicitet, spec. hos en delstrom av avloppsvatten |
US3997443A (en) * | 1975-08-21 | 1976-12-14 | Geo. A. Hormel & Co. | Apparatus for biological treatment of waste water |
JPS5226765A (en) * | 1975-08-26 | 1977-02-28 | Takenaka Komuten Co Ltd | Waste water purifying apparatus |
JPS5320652A (en) * | 1976-08-10 | 1978-02-25 | Shin Meiwa Ind Co Ltd | Rotary apparatus for aeration |
JPS5330774U (ru) * | 1976-08-24 | 1978-03-16 | ||
JPS5434544A (en) * | 1977-08-23 | 1979-03-14 | Dengyosha Mach Works | Centrifugal disk for waste water treating device and method of producing same |
JPS5643428Y2 (ru) * | 1978-03-24 | 1981-10-12 | ||
DE2919244A1 (de) * | 1979-05-12 | 1980-11-20 | Mecafina Sa | Tauchtropfkoerper fuer eine mechanisch- biologische abwasser-reinigungsanlage |
SU804576A1 (ru) * | 1979-08-01 | 1981-02-15 | Украинский Государственныйпроектный И Научно-Исследовательскийинститут Коммунальных Сооруженийгородов | Устройство дл биологическойОчиСТКи СТОчНОй жидКОСТи |
JPS5938839B2 (ja) * | 1980-08-06 | 1984-09-19 | 日立プラント建設株式会社 | 窒素含有有機性廃水の処理方法及び装置 |
US4345997A (en) * | 1981-03-09 | 1982-08-24 | Crane Co. | Media |
JPS57161496U (ru) * | 1981-04-07 | 1982-10-09 | ||
SU999214A1 (ru) | 1981-04-10 | 1992-04-30 | Производственное Объединение "Калужский Турбинный Завод" | Фильтрующий элемент |
GB8413751D0 (en) * | 1984-05-30 | 1984-07-04 | Ontario Research Foundation | Biological contact gas scrubber |
JPS61234996A (ja) * | 1985-04-09 | 1986-10-20 | Toyo Patent & Eng Kk | 嫌気性生物による汚水処理の発酵槽 |
DK157667C (da) * | 1986-05-26 | 1990-07-02 | Frandsen Aksel S | Luftdrevet kontaktfilter |
DE3903409C1 (ru) * | 1989-02-02 | 1990-05-23 | Wilhelm Prof. Dr.Phil. 1000 Berlin De Ripl | |
DE3925091A1 (de) * | 1989-07-28 | 1991-01-31 | Eberhard Dipl Biol Kuhn | Verfahren zur biologischen behandlung von abwasser und anlage sowie reaktor zur durchfuehrung des verfahrens |
RU2021214C1 (ru) | 1992-08-18 | 1994-10-15 | Павел Антонович Иващенко | Загрузка для биофильтров |
DE4441866A1 (de) * | 1994-11-17 | 1996-05-23 | Rainer Dr Hallebach | Vorrichtung zum mehrstufigen anaeroben mikrobiellen Abbau organischer Substrate |
JP2794553B2 (ja) * | 1996-03-29 | 1998-09-10 | 株式会社中国シイ・エス・ケー | 土壌菌を利用する回転接触式汚水処理装置 |
JPH1043785A (ja) * | 1996-07-30 | 1998-02-17 | Bridgestone Corp | 浴水の浄化装置 |
DE19860942C1 (de) | 1998-12-29 | 2000-05-04 | Wolfgang Luehr | Vorrichtung zur aeroben mikrobiologischen Aufbereitung von Abwasser |
JP3444349B2 (ja) * | 1999-09-20 | 2003-09-08 | 日立プラント建設株式会社 | 回転平膜装置 |
-
2001
- 2001-05-25 DE DE50110806T patent/DE50110806D1/de not_active Expired - Lifetime
- 2001-05-25 EP EP20010112677 patent/EP1260485B1/de not_active Expired - Lifetime
- 2001-05-25 AT AT01112677T patent/ATE337273T1/de not_active IP Right Cessation
-
2002
- 2002-05-24 AU AU2002339028A patent/AU2002339028B2/en not_active Ceased
- 2002-05-24 JP JP2002591401A patent/JP4632630B2/ja not_active Expired - Fee Related
- 2002-05-24 CA CA002446830A patent/CA2446830C/en not_active Expired - Fee Related
- 2002-05-24 EP EP02743096A patent/EP1390305A1/de not_active Withdrawn
- 2002-05-24 US US10/479,209 patent/US7105085B2/en not_active Expired - Fee Related
- 2002-05-24 RU RU2003137225A patent/RU2299865C2/ru not_active IP Right Cessation
- 2002-05-24 WO PCT/EP2002/005749 patent/WO2002094724A1/de active IP Right Grant
- 2002-05-24 PL PL368274A patent/PL207367B1/pl unknown
Also Published As
Publication number | Publication date |
---|---|
US20040232070A1 (en) | 2004-11-25 |
PL207367B1 (pl) | 2010-12-31 |
EP1260485A1 (de) | 2002-11-27 |
DE50110806D1 (de) | 2006-10-05 |
WO2002094724A1 (de) | 2002-11-28 |
EP1390305A1 (de) | 2004-02-25 |
JP4632630B2 (ja) | 2011-02-16 |
RU2003137225A (ru) | 2005-04-10 |
AU2002339028B2 (en) | 2007-07-26 |
CA2446830A1 (en) | 2002-11-28 |
ATE337273T1 (de) | 2006-09-15 |
JP2004524972A (ja) | 2004-08-19 |
CA2446830C (en) | 2008-11-18 |
RU2299865C2 (ru) | 2007-05-27 |
US7105085B2 (en) | 2006-09-12 |
PL368274A1 (en) | 2005-03-21 |
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